Abstract: Absorption and catalytic oxidation of nitric oxide can be achieved
by using cobalt(III) ethylenediamine (Co(en)_3^{3+}). When
simultaneous absorbing SO_2 and NO, the precipitation of
CoO_2(SO_3)_3 will be
yielded and the NO removal will be decreased. A new catalyst system using
Co(eh)_3^{3+} coupled with urea has been developed to
simultaneous remove NO and SO_2 in the flue gas. NO is
absorbed and catalytically oxidized to nitrite and nitrate by
Co(en)_3^{3+}. The dissolved oxygen in scrubbing solution
from the feed stream acts as oxidant. Urea restrains the precipitation of
CoO_2(SO_3)_3 by
oxidizing SO_3^{2-} to SO_4^{2-} as
CoSO_4 is more soluble in water. The experimental results
proved that nearly all SO_3^{2-} can be oxidized to
SO_4^{2-} and the high NO and SO_2
removal could be obtained with the new system. The NO removal is influenced by
gas flow rate, the concentration of Co(en)_3^{3+} and urea
in the absorption solution, the temperature of the scrubbing solution and the
content of oxygen in the flue gas. The low gas flow rate is favorable to
increase the NO removal. The experiments proved that the NO removal could be
maintained at more than 95% by the system of 0.02 mol/L
Co(eh)_3^{3+} and 1% urea at 50°C with 10%
O_2 in the flue gas.
Keywords: simultaneous removing SO[TeX:] _2 and NO, Co(en)[TeX:] _3^{3+}, urea, SO[TeX:] _3^{2-} oxidation